Module 10A - Heat Exchangers I
ME 524 Heat Exchangers I
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Course title: ME 524 – Air Conditioning
Institution: Kuwait University College of Engineering and Petroleum
Instructor: Dr. Ammar M. Bahman
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Lecture Outline
Types of Heat Exchangers
Overall Heat Transfer Coefficient
Fouling Factor
Analysis of Heat Exchangers
Log Mean Temperature Difference (LMTD) Method
Counter Flow Heat Exchangers
Multipass and Cross-Flow Heat Exchangers: Use of Correction Factor
Effectiveness NTU Method
Heat Exchanger Selection
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Definition of Heat Exchangers
A heat exchanger is a device that transfers thermal energy (enthalpy) between:
Two or more fluids
A solid surface and a fluid
Solid particulates and a fluid
These exchanges occur at different temperatures and in thermal contact.
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Functions of Heat Exchangers
Heating
Cooling
Evaporation
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Classification of Heat Exchangers
By Direction of Flow:
Counter Flow
Parallel Flow
Cross Flow
Hybrid Flow
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Classification by Fluid Type
Gas-to-Gas
Gas-to-Liquid (evaporator, condenser)
Liquid-to-Liquid
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Classifications Based on Flow Patterns
Single Pass
Multi Pass
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Classification by Shape & Geometry
Shell & Tube
Double Pipe
Plate Type
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Heat Exchanger Selection Criteria
Pressure limits (high/low)
Thermal performance
Temperature ranges
Pressure drops across the exchanger
Fluid flow capacity
Cost
Cleanability, maintenance, and repair
Construction materials
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Working of Tubular Type Exchanger
Components: Tube, Shell, Baffles, Tube Sheet, Inlet/Outlet for both Shell and Tube
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Shell and Tube Heat Exchanger
Most common type used in:
Oil refineries
Large chemical process plants
Consists of:
A shell (large vessel) with a bundle of tubes inside
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Types of Shell and Tube Heat Exchanger
U-Tube Heat Exchanger
Shell-side fluid flows around a tube sheet and baffles
Straight-Tube Heat Exchanger
One Pass
Tube-side configuration with multiple passes
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Tube Layout Patterns
Triangular:
Accommodates more tubes
Generates high turbulence
Suitable for clean shell side services
Square:
Required where cleaning is essential
Produces low turbulence and accommodates fewer tubes
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Components of Heat Exchangers
Channel cover
Stationary head channel
Channel flange
Pass partition plate
Tube sheet
Shell flange
Tube
Shell components
Baffles
Floating head backing device
Floating tube sheet
Floating head
Floating head flange
Stationary head bonnet
Heat exchanger support
Shell expansion joint
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Tube Sheets
Typically 100 mm thick
Forged discs and clad plates for high integrity services
Tube-to-tube sheet joints via:
Expansion of tube ends
Explosive expansion
Welding
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Double Pipe Heat Exchanger
Concentric tube heat exchanger
Fluid to be cooled/heated passes through one tube, while another fluid passes through the outer tube.
Advantages: Low design and maintenance costs
Disadvantages: Low efficiency and requires more space.
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Air Cooled Heat Exchanger (AFC)
Device for rejecting heat from fluid to ambient air
Allows placement away from water supply.
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Advantages of Air Cooled Heat Exchanger
No piping system for air is required
Larger air supply volume
No fouling/scaling
Economically favorable
Simplified maintenance
No contamination from process flow
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Disadvantages of Air Cooled Heat Exchanger
Cooling limit by ambient temperature
Increased electrical equipment
Higher initial costs
Leakage hazards
Sensitive to rain
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Components of Air Cooled Heat Exchanger
Heat transfer bundles
Air-moving device (fan or stack)
Driver for fan rotation
Support structure
Optional maintenance walkways
Louvers for temperature control
Variable pitch fan hub for savings
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Plate Heat Exchanger
Composed of multiple thin plates for large surface areas
Plates separated by rubber gaskets, arranged in troughs.
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Comparison of Heat Exchangers
Plate Type:
Higher surface area, low temperature and pressure use, suitable for non-contaminated fluids.
Tubular Type:
Designed for high-temp and pressure, lower surface area, can handle contaminated fluids.
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Problems in Heat Exchangers: Fouling
Definition: Formation of scale on heat transfer surfaces.
Effects:
Reduce heat transfer and flow
Decrease efficiency
Increase differential pressure
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Problems in Heat Exchangers: Tube Leaks
Effects:
Reduction in heat transfer
Contamination of products
Decreased efficiency
Solution: Tube replacement or plugging
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Problems in Heat Exchangers: Corrosion
Effects:
Reduced tube and shell thickness
Increased differential pressure
Decreased efficiency
Solution: Tube replacement or coating
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Monitoring in Heat Exchangers
Input/output temperature
Fluid velocity
Approach temperature
LMTD (log mean temperature difference)
Differential pressure
External leakages
Visual inspections for anomalies
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Heat Exchanger Analysis
Engineers need to:
Select heat exchangers for specified temperature changes
Predict output temperatures of fluids using two methods:
LMTD method
Effectiveness - NTU method
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Heat Transfer Principles
1st Law of Thermodynamics:
Heat transfer rate from hot fluid equals that of the cold fluid.
Equations for heat transfer relating mass flow rates and specific heats.
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Phase Change Analysis
Nomenclature for evaporation and condensation processes.
Significance of the mean temperature difference.
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Log Mean Temperature Difference Method
Essential in heat exchanger sizing.
Emphasizes the importance of using LMTD over arithmetic mean in calculations.
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Counter-Flow Heat Exchangers
Outlet temperatures and temperature differentials.
Comparison with parallel-flow exchangers regarding area and efficiency.
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Stepwise LMTD Method for Heat Exchanger Selection
Select heat exchanger type
Determine unknown temperatures and heat transfer rates
Calculate LMTD and correction factor
Select heat transfer coefficient
Calculate required surface area.
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Example Problem Using Effectiveness NTU Method
Using a counter-flow heat exchanger for water heating with geothermal fluid.
Determination of heat capacity rates and maximum heat transfer.
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Solution Steps Using Effectiveness NTU Method
Identifying heat capacity rates
Computing maximum heat transfer
Establishing effectiveness and NTU relations
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Observations from Effectiveness Relations
Insights on effectiveness ranges and economic justifications in large NTU values.
Effectiveness trends favor counter-flow configurations.
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Heat Exchanger Selection Criteria
Discusses the relationships between design decisions and operational efficiencies.